Research Article

Optimization Modeling and Empirical Research on Gasoline Octane Loss Based on Data Analysis

Table 3

The optimal operating conditions of the main operating variables.

OrderVariable codeVariable nameOptimal operating conditionsUnit

1S-ZORB.TE_2301.PVD105 temperature277.5374°C
2S-ZORB.TE_9301.PV1.0 MPa steam inlet temperature194.7160°C
3S-ZORB.FT_3301.PVDeaerated water inlet flow rate589.8554kg/h
4S-ZORB.FT_9401.PVPurify air inlet flow rate392.3236Nm3/h
5S-ZORB.FT_1004.PV3# catalytic gasoline intake flow rate37.6089T/h
6S-ZORB.AI_2903.PVOxygen content of regenerated flue gas0.9389%
7S-ZORB.LI_9102.DACAD204 liquid level45.7631%
8S-ZORB.TE_9002.DACAD203 top outlet pipe temperature29.7332°C
9S-ZORB.TE_1502.DACAD122 outlet pipe temperature44.6834°C
10S-ZORB.FT_2302.DACAD105 upper jumper loose wind flow rate102.2920Nm3/h
11S-ZORB.SIS_PT_2602.PVRegenerator top/regenerator receiver differential pressure-126.1370kPa
12S-ZORB.PDT_3602.DACACold nitrogen filter ME-114 differential pressure0.4967kPa
13S-ZORB.FT_3701.DACAClosed hopper N2 filter outlet gas flow rate25.7114Nm3/h
14S-ZORB.FT_3702.DACALock hopper H2 filter outlet gas flow rate25.4971Nm3/h
15S-ZORB.PDT_2605.DACAR-102 bottom nozzle differential pressure12.1455kPa
16S-ZORB.PDT_2906.DACAMe-108 filter differential pressure10.3282kPa
17S-ZORB.TE_7106.DACAK-101a left exhaust temperature32.1123°C
18S-ZORB.HIC_2533.AUTOMANA.OPHV2533 hand operator76.8424°C
19S-ZORB.TE_5009.DACAE-205 inlet pipe temperature27.0397°C
20S-ZORB.AT-0003.DACA.PVS-ZORB.AT-00033.0541
21S-ZORB.AT-0010.DACA.PVS-ZORB.AT-00101.0862
22S-ZORB.FT_5204.DACA.PVDegassing of gasoline products1075.6240kg/h
23S-ZORB.FT_1006.TOTALIZERA.PVHydrocracking light naphtha intake accumulated flow63021560.0446kg/h
24S-ZORB.FT_1503.DACA.PV8.0 MPa hydrogen to circulating hydrogen compressor intake flow rate2265244.5657Nm3/h
25S-ZORB.FT_1504.TOTALIZERA.PV8.0 MPa hydrogen to back blow hydrogen compressor outlet accumulated flow17278642.1169Nm3/h